The patent badge is an abbreviated version of the USPTO patent document. The patent badge does contain a link to the full patent document.

The patent badge is an abbreviated version of the USPTO patent document. The patent badge covers the following: Patent number, Date patent was issued, Date patent was filed, Title of the patent, Applicant, Inventor, Assignee, Attorney firm, Primary examiner, Assistant examiner, CPCs, and Abstract. The patent badge does contain a link to the full patent document (in Adobe Acrobat format, aka pdf). To download or print any patent click here.

Date of Patent:
Mar. 24, 2020

Filed:

Apr. 11, 2017
Applicant:

Ifp Energies Nouvelles, Rueil-Malmaison, FR;

Inventors:

Wilfried Weiss, Valencin, FR;

Elodie Tellier, Lyons, FR;

Pascal Chatron-Michaud, Lyons, FR;

Assignee:

IFP ENERGIES NOUVELLES, Rueil-Malmaison, FR;

Attorney:
Primary Examiner:
Int. Cl.
CPC ...
C10G 67/14 (2006.01); C01G 21/14 (2006.01); C10G 31/10 (2006.01); C10G 21/14 (2006.01); C10G 31/09 (2006.01); C10G 32/02 (2006.01); C10G 47/12 (2006.01); C10G 27/12 (2006.01); C10G 65/12 (2006.01); C10G 7/06 (2006.01); C10G 65/04 (2006.01); C10G 45/08 (2006.01);
U.S. Cl.
CPC ...
C10G 67/14 (2013.01); C10G 7/06 (2013.01); C10G 21/14 (2013.01); C10G 27/12 (2013.01); C10G 31/09 (2013.01); C10G 31/10 (2013.01); C10G 32/02 (2013.01); C10G 45/08 (2013.01); C10G 47/12 (2013.01); C10G 65/04 (2013.01); C10G 65/12 (2013.01); C10G 2300/1077 (2013.01); C10G 2300/202 (2013.01); C10G 2300/205 (2013.01); C10G 2300/206 (2013.01); C10G 2300/208 (2013.01);
Abstract

The invention relates to a process for the treatment of a hydrocarbon-containing feedstock making it possible to obtain a heavy hydrocarbon-containing fraction having a low sulphur content, said process comprising the following stages: a) a stage of hydrodemetallization in permutable reactors b) a stage of fixed-bed hydrotreatment of the effluent originating from stage a), c) a stage of hydrocracking in permutable reactors of the effluent originating from stage b), d) a stage of separation of the effluent originating from stage c), e) a stage of precipitation of the sediments, f) a stage of physical separation of said sediments from the heavy liquid fraction originating from stage d), g) a stage of recovery of the distillate cut used in stage e).


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